US20070243445A1 - High power density seal-less tubular solid oxide fuel cell by means of a wide interconnection - Google Patents
High power density seal-less tubular solid oxide fuel cell by means of a wide interconnection Download PDFInfo
- Publication number
- US20070243445A1 US20070243445A1 US11/403,636 US40363606A US2007243445A1 US 20070243445 A1 US20070243445 A1 US 20070243445A1 US 40363606 A US40363606 A US 40363606A US 2007243445 A1 US2007243445 A1 US 2007243445A1
- Authority
- US
- United States
- Prior art keywords
- fuel cell
- support tube
- tube
- anode
- solid oxide
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 239000000446 fuel Substances 0.000 title claims abstract description 39
- 239000007787 solid Substances 0.000 title claims abstract description 15
- 239000003792 electrolyte Substances 0.000 claims abstract description 18
- 239000007784 solid electrolyte Substances 0.000 claims abstract description 16
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Substances [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 16
- 239000000463 material Substances 0.000 claims description 9
- 239000007800 oxidant agent Substances 0.000 claims description 8
- 230000001590 oxidative effect Effects 0.000 claims description 8
- 230000005611 electricity Effects 0.000 claims description 5
- 230000000873 masking effect Effects 0.000 claims description 5
- 229910052759 nickel Inorganic materials 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims 2
- 229910052751 metal Inorganic materials 0.000 claims 2
- 239000006260 foam Substances 0.000 claims 1
- 210000004027 cell Anatomy 0.000 description 38
- 239000002001 electrolyte material Substances 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- 238000003487 electrochemical reaction Methods 0.000 description 2
- 239000007772 electrode material Substances 0.000 description 2
- 239000010405 anode material Substances 0.000 description 1
- 239000010406 cathode material Substances 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000011195 cermet Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
Images
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
- H01M8/2425—High-temperature cells with solid electrolytes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0247—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form
- H01M8/0252—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the form tubular
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/02—Details
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
- H01M8/1213—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the electrode/electrolyte combination or the supporting material
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
- H01M8/1213—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the electrode/electrolyte combination or the supporting material
- H01M8/1226—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the electrode/electrolyte combination or the supporting material characterised by the supporting layer
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
- H01M2008/1293—Fuel cells with solid oxide electrolytes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Abstract
Description
- The U.S. Government has a paid-up license in this invention and the right in limited circumstances to require the patent owner to license others on reasonable terms as provided for by the terms of DE-FC26-02NT41247 awarded by DOE.
- The field of the invention relates generally to fuel cells, and more specifically to the shape and structure of solid oxide fuel cells.
- An example of a typical solid oxide fuel cell with conductive ribs at the cathode side is shown in
FIGS. 1 and 2 . These types of solid oxide fuel cells are known in the art. The primary parts of the fuel cell are the support tube, which acts as a porous substrate only or can be made of the same material as thecathode 2 to provide an electronic media as well as porosity. Extra conductive paths can be introduced in the form ofribs 6. The number ofribs 6 will depend on the desired power output. - The
interconnection 3 provides electronic contact to the next cell in the series. Asolid electrolyte 4 is then deposited over the tubes substrate and a small portion of the interconnection. The interconnection and electrolyte provide leak tightness and prevent the fuel to mix with the air. Ananode 5 is applied over the solid electrolyte, which provides the cell active electrochemical area. Anair feed tube 7 is also included so that the air or the oxidant can be introduced to thecathode 2. - Designs may be cylindrical or flattened tubes, and comprise open or closed ended, axially elongated, ceramic tube air electrode material covered by thin film solid electrolyte and interconnection material. The electrolyte layer is covered by cermet fuel electrode material, except for a thin, axially elongated interconnection material. The flat type fuel cells comprise a flat array of electrolyte and interconnect walls or ribs, where electrolyte walls contain thin, flat layers of cathode and anode materials sandwiching an electrolyte.
- While the known fuel cells are effective the lack of good electrical contact area on the full surface of the side of the tube results in a weaker output power per cell than desired. Other embodiments of the present invention also exist, which will be apparent upon further reading of the detailed description.
- With the foregoing in mind, methods and apparatuses consistent with the present invention, which inter alia facilitates the need for greater output per cell that includes at least one flat support tube having a first and a second side, and an outer surface. The cell comprises at least one
interconnection 3 that is connected to the full surface of the outer surface of one side of the tube. The support tube comprises a solid electrolyte layer that is deposited over an outer surface of the support tube. The electrolyte also covers a portion of the interconnection layer. And, at least one anode is applied over most of the electrolyte layer. - In another embodiment, the invention is a solid oxide fuel cell that includes at least one flat support tube having a first side, a second side, and an outer surface; at least one interconnection electrically connected to the next cell in series; ribs adapted to conduct electricity about the outer surface of the support tube and an air feed tube adapted to introduce an oxidant to the support tube. The support tube comprises a solid electrolyte layer that is deposited over an outer surface of the support tube and wherein at least one anode is applied over the electrolyte. In particular embodiments at least a portion of the interconnect comprises nickel masking material about its surface.
- In yet another embodiment of the invention the solid oxide fuel cell includes at least one flat support tube having a first side, a second side, and an outer surface and at least one interconnection electrically connected to at least a majority of the surface of the outer surface of at least one side of the tube. The support tube comprises a solid electrolyte layer that is deposited over an outer surface of the support tube.
- These and other objects, features, and advantages in accordance with the present invention are provided particular embodiments by the solid oxide fuel cell of the invention. Other embodiments of the present invention also exist, which will be apparent upon further reading of the detailed description.
- The invention is explained in more detail by way of example with reference to the following drawings:
-
FIGS. 1 and 2 illustrate a known flat fuel oxide cell; and -
FIG. 3 illustrates one embodiment of the flat fuel cell of the invention. - The present invention provides for a fuel cell design that comprises at least one flat support tube having at least two sides and an outer surface. With reference to
FIG. 3 , a solid oxide fuel cell is illustrated that includes at least one flat support tube having a first and a second side, and an outer surface. The cell comprises at least oneinterconnection 3 that is deposited to the full surface of the outer surface of at least one side of the tube. The support tube comprises asolid electrolyte layer 4 that is deposited over an outer surface of the support tube. At least a portion of the interconnect is also covered with electrolyte material. At least oneanode 5 is applied over the electrolyte. - In the prior art, fuel cells employed very narrow interconnections that covered only a small portion of the outer surface of the fuel cell. By having an
interconnection 3 that covers more surface area of the outer surface of one side of the tube, optimal current distribution is achieved. In accordance with the invention, optimal current distribution is achieved by applying at least oneinterconnection 3 to at least a majority of one side so that the flat surface is completely covered up to the beginning of the curvature of each side. As used herein the term “majority” means at least 51 percent. In other words, the interconnect covers at least 51 percent of the outer surface area of one side of the support tube. “One side” refers to a flat portion of the tube and does not include the approximate area where curvature begins. This tends to equalize the current path length so that eachrib 6 would have nearly equivalent resistances. In doing so, the sides of the cell can be also consideredribs 6 as the cell has no inactivity, that is the current is flowing through all the active surface area. This increases cell performance by enhancing the electrochemical reactions at the fuel cell electrochemically active interfaces. In particular embodiments the interconnect covers up to the full outer flat surface of one side of the cell. - At least one
support cathode tube 2 comprises asolid electrolyte layer 4 that is deposited over an outer surface of the support tube. At least a portion of theinterconnect 3 is covered with electrolyte material. At least oneanode 5 is applied over the electrolyte. - This invention provides an important distinction over previous solid oxide fuel cell designs. The design provides an optimal current distribution, which enhances the power output. In accordance with the invention the interconnect is applied on one side so a majority of the outer surface of the support tube is covered by the interconnect. This results in optimal current distribution. The current path length is equalized so that each
rib 6 has nearly equivalent resistances. In doing so, the sides of the cell can be also consideredribs 6 as the cell has no inactivity. Therefore the current is optimally flowing through all the active surface area. This enhances the electrochemical reactions at the fuel cell interfaces. Previous designs allow each side to act as resistor of greater resistances, allowing the current to flow toward the path of lowest resistance and reduce the active electrochemical area. - In a specific embodiment of the invention, the interconnect completely covers at least one side of the outer surface of the support tube. The support tube of the invention is of variable length and can act as a porous substrate only or can be made of the same material as the corresponding
cathode 2 to provide an electronic media as well as porosity. The tubes may be any applicable support tube known in the art, including but not limited to flat tubes. The number ofribs 6 is dependent upon the power output. Anyone skilled in the art could determine the number of ribs to introduce without undue experimentation. - In accordance with the invention, the cell wall thickness will not exceed values where pore diffusion is comprised and cell performance is lowered. The
rib 6 to wall interfaces will have a radius, and the closed end with be ellipsoidal in nature. - In another embodiment the present invention includes at least one flat support tube having a first and a second side, and an outer surface. The cell comprises at least one
interconnection 3 that is connected to the full surface of the outer surface of at least one side of the tube. The support tube comprises a solid electrolyte layer that is deposited over an outer surface of the support tube. At least a portion of the interconnect is covered with electrolyte material, and at least one anode is applied over the electrolyte. - In another embodiment, the invention is a solid oxide fuel cell that includes at least one flat support tube having a first side, a second side, and an outer surface; at least one interconnection electrically connected to the full surface of the outer surface of at least one side of the tube; ribs adapted to conduct electricity about the outer surface of the support tube and an air feed tube are adapted to introduce an oxidant to the support tube. The support tube comprises a solid electrolyte layer that is deposited over an outer surface of the support tube and wherein at least one anode is applied over the electrolyte.
- In yet another embodiment of the invention the solid oxide fuel cell includes at least one flat support tube having a first side, a second side, and an outer surface and at least one interconnection deposited to at least a majority of the surface of the outer surface of at least one side of the tube. The support tube comprises a solid electrolyte layer that is deposited over an outer surface of the support tube. At least one anode is applied over the electrolyte.
- The
anode 5 is applied over the solid electrolyte. Theanode 5 provides the cell active electrochemical area. Usually cylindrical cells are connected into bundles by means of an electrical connection made of nickel felts, screen, or screen and felt combinations. In one embodiment of the invention air or the oxidant is introduced to the cathode by means of an air feed tube. - While specific embodiments of the invention have been described in detail, it will be appreciated by those skilled in the art that various modifications and alternatives to those details could be developed in light of the overall teachings of the disclosure. Accordingly, the particular arrangements disclosed are meant to be illustrative only and not limiting as to the scope of the inventions which, is to be given the full breadth of the claims appended and, any and all equivalents thereof.
Claims (14)
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/403,636 US20070243445A1 (en) | 2006-04-13 | 2006-04-13 | High power density seal-less tubular solid oxide fuel cell by means of a wide interconnection |
PCT/US2006/045839 WO2007133260A1 (en) | 2006-04-13 | 2006-11-30 | High power density seal-less tubular solid oxide fuel cell by means of a wide interconnection |
JP2009505352A JP2009533819A (en) | 2006-04-13 | 2006-11-30 | High power density sealless tubular solid oxide fuel cell with wide interconnects |
EP06849909A EP2005508A1 (en) | 2006-04-13 | 2006-11-30 | High power density seal-less tubular solid oxide fuel cell by means of a wide interconnection |
KR1020087027813A KR20080109930A (en) | 2006-04-13 | 2006-11-30 | High power density seal-less tubular solid oxide fuel cell by means of a wide interconnection |
CA002649079A CA2649079A1 (en) | 2006-04-13 | 2006-11-30 | High power density seal-less tubular solid oxide fuel cell by means of a wide interconnection |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/403,636 US20070243445A1 (en) | 2006-04-13 | 2006-04-13 | High power density seal-less tubular solid oxide fuel cell by means of a wide interconnection |
Publications (1)
Publication Number | Publication Date |
---|---|
US20070243445A1 true US20070243445A1 (en) | 2007-10-18 |
Family
ID=38521218
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/403,636 Abandoned US20070243445A1 (en) | 2006-04-13 | 2006-04-13 | High power density seal-less tubular solid oxide fuel cell by means of a wide interconnection |
Country Status (6)
Country | Link |
---|---|
US (1) | US20070243445A1 (en) |
EP (1) | EP2005508A1 (en) |
JP (1) | JP2009533819A (en) |
KR (1) | KR20080109930A (en) |
CA (1) | CA2649079A1 (en) |
WO (1) | WO2007133260A1 (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090123810A1 (en) * | 2007-11-08 | 2009-05-14 | Alan Devoe | Fuel cell device and system |
US20100009228A1 (en) * | 2008-07-08 | 2010-01-14 | Siemens Power Generation, Inc. | Solid oxide fuel cell with transitioned cross-section for improved anode gas management at the open end |
US20100009091A1 (en) * | 2008-07-08 | 2010-01-14 | Siemens Power Generation, Inc. | Fabrication of Copper-Based Anodes Via Atmosphoric Plasma Spraying Techniques |
US8293417B2 (en) | 2006-11-08 | 2012-10-23 | Alan Devoe | Solid oxide fuel cell device |
US8715879B2 (en) | 2007-05-10 | 2014-05-06 | Alan Devoe | Fuel cell device and system |
US8932776B2 (en) | 2006-05-11 | 2015-01-13 | Alan Devoe | Solid oxide fuel cell device and system |
US8962209B2 (en) | 2008-03-07 | 2015-02-24 | Alan Devoe | Fuel cell device and system |
US9023555B2 (en) | 2012-02-24 | 2015-05-05 | Alan Devoe | Method of making a fuel cell device |
US9059450B2 (en) | 2008-10-28 | 2015-06-16 | Alan Devoe | Fuel cell device and system |
US9209474B2 (en) | 2009-03-06 | 2015-12-08 | Alan Devoe | Fuel cell device |
US9437894B2 (en) | 2012-02-24 | 2016-09-06 | Alan Devoe | Method of making a fuel cell device |
US20190081331A1 (en) * | 2015-12-28 | 2019-03-14 | Robert Bosch Gmbh | Method for producing a flow plate for a fuel cell |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4874678A (en) * | 1987-12-10 | 1989-10-17 | Westinghouse Electric Corp. | Elongated solid electrolyte cell configurations and flexible connections therefor |
US6440596B1 (en) * | 1999-10-20 | 2002-08-27 | Technology Management, Inc. | Solid-oxide fuel cell hot assembly |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3102809B2 (en) * | 1991-05-20 | 2000-10-23 | 日本電信電話株式会社 | Hollow thin plate solid electrolyte fuel cell |
US6416897B1 (en) * | 2000-09-01 | 2002-07-09 | Siemens Westinghouse Power Corporation | Tubular screen electrical connection support for solid oxide fuel cells |
JP4146738B2 (en) * | 2002-02-07 | 2008-09-10 | 京セラ株式会社 | Fuel cell, cell stack and fuel cell |
JP4018916B2 (en) * | 2002-03-14 | 2007-12-05 | 京セラ株式会社 | Fuel cell, cell stack and fuel cell |
US7285348B2 (en) * | 2003-02-28 | 2007-10-23 | Kyocera Corporation | Fuel cell |
-
2006
- 2006-04-13 US US11/403,636 patent/US20070243445A1/en not_active Abandoned
- 2006-11-30 WO PCT/US2006/045839 patent/WO2007133260A1/en active Application Filing
- 2006-11-30 EP EP06849909A patent/EP2005508A1/en not_active Withdrawn
- 2006-11-30 KR KR1020087027813A patent/KR20080109930A/en not_active Application Discontinuation
- 2006-11-30 CA CA002649079A patent/CA2649079A1/en not_active Abandoned
- 2006-11-30 JP JP2009505352A patent/JP2009533819A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4874678A (en) * | 1987-12-10 | 1989-10-17 | Westinghouse Electric Corp. | Elongated solid electrolyte cell configurations and flexible connections therefor |
US6440596B1 (en) * | 1999-10-20 | 2002-08-27 | Technology Management, Inc. | Solid-oxide fuel cell hot assembly |
Cited By (35)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10673081B2 (en) | 2005-11-08 | 2020-06-02 | Alan Devoe | Solid oxide fuel cell device |
US9673459B2 (en) | 2005-11-08 | 2017-06-06 | Alan Devoe | Solid oxide fuel cell device |
US10096846B2 (en) | 2005-11-08 | 2018-10-09 | Alan Devoe | Solid oxide fuel cell device |
US8932776B2 (en) | 2006-05-11 | 2015-01-13 | Alan Devoe | Solid oxide fuel cell device and system |
US10559839B2 (en) | 2006-05-11 | 2020-02-11 | Alan Devoe | Solid oxide fuel cell device and system |
US9859582B2 (en) | 2006-05-11 | 2018-01-02 | Alan Devoe | Solid oxide fuel cell device and system |
US9397346B2 (en) | 2006-11-08 | 2016-07-19 | Alan Devoe | Solid oxide fuel cell device |
US8293417B2 (en) | 2006-11-08 | 2012-10-23 | Alan Devoe | Solid oxide fuel cell device |
US8609290B2 (en) | 2006-11-08 | 2013-12-17 | Alan Devoe | Solid oxide fuel cell device |
US9123937B2 (en) | 2006-11-08 | 2015-09-01 | Alan Devoe | Solid oxide fuel cell device |
US10312530B2 (en) | 2007-05-10 | 2019-06-04 | Alan Devoe | Fuel cell device and system |
US8715879B2 (en) | 2007-05-10 | 2014-05-06 | Alan Devoe | Fuel cell device and system |
US9362572B2 (en) | 2007-05-10 | 2016-06-07 | Alan Devoe | Fuel cell device and system |
US10153496B2 (en) | 2007-11-08 | 2018-12-11 | Alan Devoe | Fuel cell device and system |
US8614026B2 (en) | 2007-11-08 | 2013-12-24 | Alan Devoe | Fuel cell device and system |
US8227128B2 (en) * | 2007-11-08 | 2012-07-24 | Alan Devoe | Fuel cell device and system |
US20090123810A1 (en) * | 2007-11-08 | 2009-05-14 | Alan Devoe | Fuel cell device and system |
US9343753B2 (en) | 2008-03-07 | 2016-05-17 | Alan Devoe | Fuel cell device and system |
US8962209B2 (en) | 2008-03-07 | 2015-02-24 | Alan Devoe | Fuel cell device and system |
US8097384B2 (en) | 2008-07-08 | 2012-01-17 | Siemens Energy, Inc. | Solid oxide fuel cell with transitioned cross-section for improved anode gas management at the open end |
US20100009228A1 (en) * | 2008-07-08 | 2010-01-14 | Siemens Power Generation, Inc. | Solid oxide fuel cell with transitioned cross-section for improved anode gas management at the open end |
US20100009091A1 (en) * | 2008-07-08 | 2010-01-14 | Siemens Power Generation, Inc. | Fabrication of Copper-Based Anodes Via Atmosphoric Plasma Spraying Techniques |
US8163353B2 (en) | 2008-07-08 | 2012-04-24 | Siemens Energy, Inc. | Fabrication of copper-based anodes via atmosphoric plasma spraying techniques |
US10734659B2 (en) | 2008-10-28 | 2020-08-04 | Alan Devoe | Fuel cell device and system |
US9059450B2 (en) | 2008-10-28 | 2015-06-16 | Alan Devoe | Fuel cell device and system |
US10062911B2 (en) | 2008-10-28 | 2018-08-28 | Alan Devoe | Fuel cell device and system |
US9209474B2 (en) | 2009-03-06 | 2015-12-08 | Alan Devoe | Fuel cell device |
US10320012B2 (en) | 2011-11-30 | 2019-06-11 | Alan Devoe | Fuel cell device |
US9716286B2 (en) | 2012-02-24 | 2017-07-25 | Alan Devoe | Method of making a fuel cell device |
US10355300B2 (en) | 2012-02-24 | 2019-07-16 | Alan Devoe | Method of making a fuel cell device |
US9023555B2 (en) | 2012-02-24 | 2015-05-05 | Alan Devoe | Method of making a fuel cell device |
US9577281B1 (en) | 2012-02-24 | 2017-02-21 | Alan Devoe | Method of making a fuel cell device |
US9437894B2 (en) | 2012-02-24 | 2016-09-06 | Alan Devoe | Method of making a fuel cell device |
US20190081331A1 (en) * | 2015-12-28 | 2019-03-14 | Robert Bosch Gmbh | Method for producing a flow plate for a fuel cell |
US10903507B2 (en) * | 2015-12-28 | 2021-01-26 | Robert Bosch Gmbh | Method for producing a flow plate for a fuel cell |
Also Published As
Publication number | Publication date |
---|---|
EP2005508A1 (en) | 2008-12-24 |
JP2009533819A (en) | 2009-09-17 |
WO2007133260A1 (en) | 2007-11-22 |
KR20080109930A (en) | 2008-12-17 |
CA2649079A1 (en) | 2007-11-22 |
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